US5590958A - Automatic cementing system for precisely obtaining a desired cement density - Google Patents

Automatic cementing system for precisely obtaining a desired cement density Download PDF

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US5590958A
US5590958A US08470976 US47097695A US5590958A US 5590958 A US5590958 A US 5590958A US 08470976 US08470976 US 08470976 US 47097695 A US47097695 A US 47097695A US 5590958 A US5590958 A US 5590958A
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Prior art keywords
slurry
chamber
cement
system
rate
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Expired - Lifetime
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US08470976
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Michael P. Dearing, Sr.
Robert A. Baten
Greg L. Cedillo
Bruce A. Vicknair
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JP Morgan Chase Bank
Stewart and Stevenson LLC
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Steward and Stevenson Services Inc
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    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/25Methods for stimulating production
    • E21B43/26Methods for stimulating production by forming crevices or fractures
    • E21B43/267Methods for stimulating production by forming crevices or fractures reinforcing fractures by propping
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING, DISPERSING
    • B01F15/00Accessories for mixers ; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F15/00123Controlling; Testing; Measuring
    • B01F15/00129Measuring operational parameters
    • B01F15/00155Measuring the level of material in a container or the position or shape of the upper surface of the material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING, DISPERSING
    • B01F15/00Accessories for mixers ; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F15/00123Controlling; Testing; Measuring
    • B01F15/00207Measuring properties of the mixtures, e.g. temperature, density, colour, vibration, noise
    • B01F15/00233Measuring density or solids or particle number
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING, DISPERSING
    • B01F15/00Accessories for mixers ; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F15/04Forming a predetermined ratio of the substances to be mixed
    • B01F15/0408Adding a component to a mixture in response to a detected feature, e.g. density, radioactivity, consumed power, colour
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28CPREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C7/00Controlling the operation of apparatus for producing mixtures of clay or cement with other substances; Supplying or proportioning the ingredients for mixing clay or cement with other substances; Discharging the mixture
    • B28C7/02Controlling the operation of the mixing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28CPREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C7/00Controlling the operation of apparatus for producing mixtures of clay or cement with other substances; Supplying or proportioning the ingredients for mixing clay or cement with other substances; Discharging the mixture
    • B28C7/02Controlling the operation of the mixing
    • B28C7/022Controlling the operation of the mixing by measuring the consistency or composition of the mixture, e.g. with supply of a missing component
    • B28C7/024Controlling the operation of the mixing by measuring the consistency or composition of the mixture, e.g. with supply of a missing component by measuring properties of the mixture, e.g. moisture, electrical resistivity, density
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00Moulds or cores; Details thereof or accessories therefor
    • B29C33/44Moulds or cores; Details thereof or accessories therefor with means for, or specially constructed to facilitate, the removal of articles, e.g. of undercut articles
    • B29C33/442Moulds or cores; Details thereof or accessories therefor with means for, or specially constructed to facilitate, the removal of articles, e.g. of undercut articles with mechanical ejector or drive means therefor
    • B29C33/444Moulds or cores; Details thereof or accessories therefor with means for, or specially constructed to facilitate, the removal of articles, e.g. of undercut articles with mechanical ejector or drive means therefor for stripping articles from a mould core, e.g. using stripper plates
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B47/00Survey of boreholes or wells
    • E21B47/0005Survey of boreholes or wells control of cementation quality or level
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D21/00Control of chemical or physico-chemical variables, e.g. pH value
    • G05D21/02Control of chemical or physico-chemical variables, e.g. pH value characterised by the use of electric means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING, DISPERSING
    • B01F3/00Mixing, e.g. dispersing, emulsifying, according to the phases to be mixed
    • B01F3/12Mixing, e.g. dispersing, emulsifying, according to the phases to be mixed liquids with solids
    • B01F2003/125Mixing, e.g. dispersing, emulsifying, according to the phases to be mixed liquids with solids by introducing, e.g. dispersing, dissolving, solids in liquids

Abstract

An automatic cementing system and method are disclosed for precisely controlling the density of a slurry during a continuously mixed cement application. The system includes an input water line and a dry cement hopper for supplying water and dry cement, respectively, to a mixing chamber. The mixing chamber includes two chambers, Chamber A and Chamber B, for thoroughly mixing the water and cement together to form a cement slurry. Chamber B includes a level sensor for measuring the change in slurry level. The input line includes a pump for supplying the water to the mixing chamber, and a flow meter for measuring the rate at which the water is supplied. Similarly, the hopper includes a rotary valve for regulating the rate at which the dry cement is supplied to the mixing chamber and a speed sensor for measuring the speed of the rotary valve. A discharge line with a discharge pump and a discharge flow meter receives and discharges cement slurry. A recirculation line is included for density control during initialization. A system controller receives operational parameters from the operator, including desired slurry density, mix water density and dry cement density. Once the rate of the input pump is set, the controller monitors the output from the level sensor in Chamber B and adjusts the rotary valve until the level of slurry in Chamber B is constant. At that time,, the amount of water leaving the system as slurry is calculated by the controller, and the controller then sets the rate of the input pump based upon this calculation.

Description

BACKGROUND OF THE INVENTION

This is a divisional continuing application of copending application U.S. Ser. No. 08/178,659, filed Jan. 7, 1994, which is a continuation-in-part of U.S. Ser. No. 07/969,944, filed Oct. 30, 1992 (now abandoned), which was a divisional of then U.S. Ser. No. 07/389,923, filed Aug. 2, 1989 (now U.S. Pat. No. 5,281,023).

The invention disclosed herein relates generally to an apparatus and method for obtaining a slurry with a desired density during a continuous-mixing operation. More particularly, the invention relates to an automated system for automatically controlling the density of a cement slurry with a very high degree of precision for use in well completions.

Systems for mixing dry cement with water are well known in the art. Typically, cement mixing for large jobs is either done by batch-mixing or by continuous-mixing. A batch-mixing operation occurs when the ingredients are mixed in a large tank or blender to obtain the entire volume of cement slurry before the start of the job. A continuous-mixing job, conversely, is an operation in which the ingredients are continuously mixed during the course of the job to produce a slurry for immediate use. The advantages of batch-mixing cement is that the density can be controlled very accurately. The disadvantage is that batch-mixing may prove to be impossible or impractical on large jobs in which a large volume of cement slurry must be generated. Because the slurry is premixed in a batch job, a blender or tank must be provided that is large enough to hold all of the slurry to be used on that particular job. Continuous mixing alleviates this problem, in that the slurry is mixed "on the fly" in a relatively small mixing chamber and is used immediately.

One problem, however, with continuously mixing the slurry is that it is very difficult to control the density of the slurry with any decree of precision because ingredients are constantly being added and slurry is constantly being discharged. As a result, it is common to have fluctuations in slurry density during continuous-mix operations. In certain applications, cement density fluctuation can cause severe problems. One example where cement density fluctuations are particularly undesirable is in cementing operations for casing a wellbore. The density of cement is especially critical for such cementing operations.

Cement is used in wells to secure casing in place in a wellbore to "complete" the well. The purpose of the cement is to seal and block various zones between the casing and the wellbore. Special additives may be mixed with the cement to alter specific properties of the cement, as required by the wellbore and casing characteristics and relationships. A general overview of cementing casing may be found in Skinner, D. R., Introduction to Petroleum Production, Volume I, Chapter 4: Well Completion (Gulf Publishing Co. 1981), and in Moore, Preston L., Drilling Practices Manual, Chapter 16 (PennWell Publishing Co. 1974).

Several terms commonly are used in cementing operations, as follows:

Cement Slurry refers to the mixture of dry or powdered cement and water that is injected or pumped into the wellbore;

Slurry volume refers to the volume of slurry that is obtained when a given volume of dry cement is mixed with a given volume of water; and

Slurry density refers to the amount of dry cement per volume of water, and typically is measured in terms of pounds per gallon (also referred to as "PPG");

Different cements cure in different ways; for example, some cements expand as they cure, while others shrink. During the curing process, cement generally increases in temperature. Some cement mixtures will crack or become increasingly permeable as a result of this increase in temperature during the curing process. Because the heat of the earth increases at greater depths, cracking of the cement becomes more pronounced as the depth of the wellbore increases if cement is used downhole in wells.

The cement and water typically are mixed on site during a cementing operation because most wells are located in remote locations where it is impractical to use large mixing tanks. Such an application commonly is referred to as a continuous-mixing job. The materials used in the cement are usually prepared dry and transported to the well site, where it is mixed with liquid or "mix water" and pumped into the well. Various dry or liquid additives also may be added to either the mix water or to the dry cement as desired to alter the properties of the cement slurry. The cement slurry normally is pumped in liquid form into a wellbore by pumping the slurry down the interior of the casing and forcing the slurry to flow from the bottom of the casing back upward between the casing and the wellbore. After the cement has been pumped into the wellbore, it must be allowed to cure for a certain period of time that can vary between 12-72 hours.

By evaluating the wellbore and formation characteristics, a person skilled in the art can determine with a good deal of precision the preferred cement density to use during the cement job to most effectively protect the casing and separate producing formations. If a cement slurry density could be maintained within a tight tolerance of ±0.1 lbs/gallon (PPG) of the preferred density, the probability of a successful cementing operation would be much higher. Some authors have stated that proper mixing of the cement slurry is critical to successful completion of a cementing job on a well, and have proposed systems to alleviate this problem with density control in continuous-mixing operations. See e.g. Galiana, et. al., "Cement Mixing: Better Understanding and New Hardware," Oilfield Review, (April 1991); Hitt, et. al., "Process Control of Slurry Density: Impact on Field Performance of Slurry Density," presented at the Society of Petroleum Engineers' Production Operations Symposium held in Oklahoma City, Okla., Apr. 7-9, 1991; O'Neill, et. al., "New Slurry Mixer Improves Density Control in Cementing Operations," presented at the Society of Petroleum Engineers' Latin America Petroleum Engineering Conference held in Rio de Janeiro, Oct. 14-19, 1990; Wienck, et. al., "Automatic Control of Bulk Cement Tank Levels," presented at the 24th Annual Offshore Technology Conference in Houston, Tex., May 4-7 1992; and Stegemoeller, et. al., "Automatic Density Control and High Specific Mixing Energy Deliver Consistent High-Quality Cement Slurries," presented at the 24th Annual Offshore Technology Conference in Houston, Tex., May 4-7, 1992.

Unfortunately, the prior art continuous-mix cementing systems have been unable to guarantee the density of the cement slurry within an acceptable tolerance level. Most prior art cementing systems are subject to a wide fluctuation in cement slurry density. See the discussion in Galiana, et. al., "Cement Mixing: Better Understanding and New Hardware," Oilfield Review, (April 1991). Even the systems developed more recently have encountered difficulty in obtaining a slurry density within ±0.1 lbs/gallon. Id. One of the reasons for this variance is that the meters and valves used in the mixing and density control systems typically are designed to be within a predetermined accuracy. Consequently, a certain amount of error is common in most meters. This is especially true with respect to the dry cement delivery system. Compounding this problem is the fact that many density control systems attempt to obtain a desired density by fixing the amount of dry cement to be delivered, while adjusting the rate at which water is input based upon feedback from a density sensor. See e.g. Stegemoeller, et. al. "Automatic Density Control and High Specific Mixing Energy Deliver Consistent High-Quality Cement Slurries," presented at the 24th Annual Offshore Technology Conference in Houston, Tex., May 4-7, 1992. The meters and valves associated with the dry cement delivery system have a relatively large error associated with them that makes any control system suspect that is based upon setting the delivery of dry cement to a fixed level. This error results from a number of factors such as the tendency of the dry cement to coagulate. Because of the difficulty in handling and supplying dry cement during a cementing operation, it is very difficult to maintain a constant slurry density.

Because of the inherent inaccuracy in all of the meters and valves typically used in an automatic density system, and especially those related to the dry cement delivery system, it is extremely difficult to design a system that can very accurately and precisely control the density of a cement slurry. It is an object of the present invention to automatically control the density of the cement slurry obtained in a continuous-mixing application to within ±0.1 lbs/gallon (PPG) of the desired density for cementing operations that is relatively independent of the error inherent in the meters and valves used in the system and especially those related to the dry cement delivery system.

SUMMARY OF THE INVENTION

The present invention comprises a system and method for automatically and precisely controlling the density of a cement slurry, which preferably includes a fresh water input device, such as a pump or a valve, and a dry cement delivery system, supplying mix water and cement, respectively, to a mixing chamber. The mixing chamber combines the mix water and cement to obtain a cement slurry that is discharged through a discharge line to a well or other desired location. The rate and amount of slurry being discharged is measured by a discharge flow meter. The input mix water line includes a flow meter and the dry cement delivery system includes a valve or other device for regulating the amount of dry cement delivered to the mixing chamber.

The system controller also preferably receives as inputs from an operator (1) the desired or target slurry density in pounds per gallon (PPG); (2) the density of the input mix water in specific gravity units; and (3) the absolute density of the dry cement, in specific gravity units.

The discharge line of the system preferably includes a discharge valve and a discharge flow meter. The discharge flow meter provides an indication of the rate at which slurry is being discharged. With this information, and the information provided by the operator, the controller determines the percent by volume of dry cement in the cement slurry. In other words, the controller determines how much dry cement is leaving the system as part of the cement slurry. Once the percent by volume of dry cement is known, the controller then determines the percent by volume of liquid in the cement slurry. After the controller determines the percent by volume of liquid in the slurry, the controller calculates the amount of liquid that must be supplied to the system through the input line by multiplying the discharge rate by the percent by volume of liquid in the slurry. In this manner, the controller insures that the same amount of liquid is flowing into the system as is flowing out as a component of the cement slurry. Once the controller determines the proper input rate of liquid into the system, the controller adjusts the input pump or input valve to provide the mix water at the required rate. The input flow meter is used as feedback to bring the input water device to the proper speed or position.

After the input device is set at the proper speed or position, the controller sets an approximate speed or position for the valve to control the delivery of dry cement. The controller uses the percent by volume of cement in the slurry and the discharge rate, together with other factors, to determine the desired quantity of dry cement to deliver. The controller then compares the desired quantity of dry cement to be delivered with the measured valve and modifies the valve as necessary to modify the delivery of dry cement.

The mixing chamber preferably comprises a divided tub, with Chambers A and B, for receiving water and dry cement, with the discharge line connected to the chamber B. In addition, a tub level sensor is provided to monitor the change in slurry level in chamber B. After setting the approximate speed of the dry cement valve, the controller adjusts the speed or position of the valve to precisely control the amount of dry cement supplied to the mixing chamber, based upon the level sensor. The controller continues to adjust the speed or position of the valve until the level of slurry in chamber B remains constant.

The invention also preferably includes a recirculation line to permit the density of the slurry to be brought to the desired density before it is discharged, and before automatic operation begins. The recirculation line includes a density meter for measuring the density of the cement slurry and for providing an indication of that density to the system controller.

These and other advantages and details of the invention will become apparent from a review of the Detailed Description which follows.

BRIEF DESCRIPTION OF THE DRAWINGS

For a detailed description of the preferred embodiment of the invention, reference will be made now to the accompanying drawings, wherein:

FIG. 1 is a schematic illustration of the configuration of the Automatic Cementing System of the preferred embodiment.

FIGS. 2A-2F illustrates a flow chart of the operation of the ACS system of FIG. 1.

FIG. 3 shows a flow chart of the dry feed interrupt for controlling the valve of the dry cement delivery system of FIG. 1.

FIG. 4 shows a flow chart of the mix water interrupt for controlling the rate at which fluid is supplied to the mixing chamber of FIG. 1.

FIG. 5 is a flow chart showing how the rate and total volume of the mix water is generated.

FIG. 6 is a flow chart showing how the rate and total volume of slurry discharged is generated.

FIG. 7 is a flow chart showing how the rate of the dry cement is generated.

DESCRIPTION OF THE PREFERRED EMBODIMENT

Referring now to FIG. 1, the Automatic Cementing System 10 constructed in accordance with the preferred embodiment generally comprises an input (or "mix") water supply line 30, a dry cement source 40 for supplying dry cement, a mixing chamber 60 for mixing dry cement and water, a cement slurry discharge line 80, a recirculating slurry line 90, and a system controller 100 for receiving output signals from the various system components and for providing control signals to regulate the operation of the ACS system.

The input water supply line 30 preferably provides mix water (or other base liquid) to the mixing chamber 60 for mixing with the dry cement from source 40. The water supply line 30 preferably includes a fresh water pump 35, an input flow meter 37, and a mixing bowl 55 for receiving dry cement from hopper 51. Alternatively, a centrifugal pump (not shown) may be used with an input valve instead of a positive displacement pump. Similarly, mixing of the cement and water can take place in a jet mixer instead of a mixing bowl 55. The water/cement mixture preferably flows from mixing bowl 55 (or jet mixer) into mixing chamber 60.

In the preferred embodiment, the pump 35 comprises a positive displacement pump, while the input flow meter 37 comprises mag-type flow meter. The pump 35 (or input valve, in the alternative embodiment) preferably connects electrically to the system controller 100 for receiving control signals. The input flow meter 37 preferably connects electrically to the system controller 100 and provides an electrical signal to the controller 100 that is indicative of the flow rate of mix water into the mixing chamber 60. Preferably, the input flow meter has an accuracy of 0.50%. The water supply line 30 preferably connects to a fresh water supply (not shown), which may be mounted on a truck, or which may comprise a water tower or other available water source capable of generating the required volume at the requisite rate.

The apparatus for providing dry or powdered cement to the mixing chamber 60 preferably comprises a hopper 51 that includes a supply conduit 41, a weight sensor 44, a valve 45 in combination with a valve sensor 47, and a vibrator motor 49. As one skilled in the art will immediately realize, many other delivery systems may be used without departing from the principles of this invention. For example, an air slide may be used instead of the vibrator to insure uninterrupted flow of cement into the valve 45. The hopper 51 receives the dry cement

through conduit 41, which connects the hopper 51 to a source of dry cement (not shown). In accordance with conventional techniques, dry additives may be combined with dry cement either before or during the cement operation. In addition, to insure a good flow of dry cement through conduit 41, the dry cement preferably is blown through conduit 41. The conduit 41 preferably includes a cement inlet control valve 42 that connects electrically to the system controller 100 and which receives control signals from the controller 100. In response to the control signals from controller 100, the inlet control valve is positioned to regulate the amount of dry cement supplied to the hopper 51. As noted, the hopper 51 also preferably includes a weight sensor 44 for determining the amount of cement in the hopper 51 by weight. Weight sensor 44, which preferably comprises a load cell, also connects electrically to the system controller 100 for providing an electrical signal to the controller 100 that represents the weight, and thus the amount, of dry cement in hopper 51.

Valve 45, or other suitable regulating device, controls the amount of cement that is delivered to mixing bowl 55. In accordance with conventional techniques, the dry cement is dropped on top of the water being injected through input line 30, at mixing bowl 55. Although not required in the preferred embodiment, a jet nozzle (not shown) may be provided on the input line 30, just upstream from the mixing bowl 55. The cement/water mixture then flows into the mixing chamber 60 where further mixing occurs. Other alternative mixing, arrangements cab be used, however, without departing from the principles of the present invention.

In the preferred embodiment, the valve 45 comprises a rotary or "star wheel" valve, with a controller 46 that can be externally regulated. The controller 46 of valve 45 preferably connects electrically to the system controller 100 for receiving electrical signals that are used to regulate the speed (or position if the valve is not a rotary valve) of valve 45 in order to control the rate at which dry cement is delivered to the mixing chamber 60. Sensor 47 preferably comprises a star wheel speed sensor for measuring the speed of rotary valve 45. In addition, sensor 47 preferably connects electrically to the system controller 100 to provide an electrical signal to system controller 100 that is indicative of the speed (or position) of valve 45. As will be understood by one skilled in the art, various other valves, controllers and sensors could be used without departing from the principles of the present invention. For example, a slide gate may be used in place of a rotary valve. The position of the slide gate then would be monitored to determine the size of the opening through which cement could pass.

The mixing chamber 60 receives mix water from the input supply line 30 and dry or powdered cement from the dry cement hopper 51, and mixes the water and dry cement to obtain a cement slurry. Other chemicals or additives also may be supplied to the mixing chamber 60, as desired. Mixing chamber 60 preferably includes two divided chambers, Chamber A and Chamber B, to define a weir divider for removing entrained air according to well known principles. Both Chamber A and Chamber B include a mixer for mixing the cement and water.

The mixing chamber 60 preferably is constructed so that the cement and water pour into Chamber A when it is first mixed. As Chamber A becomes full, the slurry pours over into Chamber B. The discharge line 80 preferably connects to the lower side of Chamber B. In the preferred embodiment, a tub level sensor 65 is provided for measuring the slurry level of Chamber B. This tub level sensor 65 preferably comprises a sonic level sensor, and Chamber B is constructed so that it is relatively deep, while having a relatively small cross-section area. Obviously, other dimensions could also be used without departing from the principles of the present invention. By constructing Chamber B with a relatively small cross-section, changes in slurry level in Chamber B will be more pronounced, and thus will be more easily detected by the level sensor 65.

The discharge line 80 preferably receives cement slurry from the lower side of Chamber B and supplies the slurry to the well site. The discharge line 80 includes a discharge flow meter 87 for measuring the rate at which slurry is discharged, a manually controlled discharge pump 82, and a discharge valve 85. In the preferred embodiment, the discharge flow meter 87 comprises a non-intrusive sensor, such as a magnetic flow meter, capable of an accuracy within 0.5%. The discharge flow meter 87 preferably connects electrically to the system controller 100 to provide an output signal that is indicative of the flow rate of cement slurry through discharge line 80. The discharge pump 82 preferably comprises a centrifugal pump that is manually controlled by the operator. One or more triplex pumps 89 also may be provided downstream in the slurry discharge line 80 in accordance with conventional techniques. The triplex pumps are manually regulated by the operator and normally are run at full speed.

The discharge valve 85 works in conjunction with recirculation line 90. When discharge valve 85 is closed, cement slurry is forced to flow through the recirculation line 90. The recirculation line 90 preferably connects between the discharge line 80 and the mixing bowl 55. The recirculation 90 preferably performs two separate functions. First, the recirculation line 90 enables the system to bring the cement slurry to the desired density before discharging begins. Second, during the time cement is being discharged, the amount of slurry recirculated is regulated by the recirculation valve 97. This recirculated slurry adds energy to the mixing process in the mixing bowl 55 and tends to dampen slurry density fluctuations in the mixing chamber 60. The recirculation valve 97 is a throttling type valve and regulates the amount of slurry recirculated. It is used in conjunction with pump 82 speed control to control the discharge pressure in line 80. In the preferred embodiment, a nuclear density meter 95, which preferably has an accuracy within ±0.1 PPG for precisely measuring the density of the cement slurry, is preferably located immediately downstream from pump 82 and before the recirculation line connection.

Alternatively, one skilled in the art will understand that the present invention can be used without a recirculation line or alternatively, no density meter need be included. If no density meter is included, then the density of the cement slurry may still be obtained through the use of the input flow meter and discharge flow meter, as disclosed in parent application, U.S. Ser. No. 07/969,944, the teachings of which are incorporated herein. Alternatively, the density of the slurry may be measured by taking sample readings.

The system controller 100 preferably comprises a microprocessor-based unit for orchestrating the operation of the ACS system. In the preferred embodiment, Motorola's 68HC11 is used as the microprocessor. The controller 100 preferably includes an input, such as a keyboard or operator panel, through which system parameters can be input by an operator. The controller 100 also preferably includes an output for displaying to the operator certain critical system parameters. Preferably, the input and output of the controller 100 are designed so that the operator is guided by a menu driven display to insure that all necessary information is provided by the operator.

Also in the preferred embodiment, the system controller 100 may include one or more read-only memory (ROM) units for storing look-up tables that are loaded into the controller 100 prior to the start of a cement job. These look-up values are used to correlate step rates with error values for both the mix water rate and the dry cement delivery rate. Thus, for example, if the desired mix water rate is different than the actual mix water rate, as measured by input flow meter 37, an error value is calculated by controller 100 based upon the difference. The controller 100 then accesses the look-up table, which preferably is stored on ROM, to determine the appropriate step rate by which the mix water rate should be changed. The step rate, therefore, determines how quickly the rate increases or decreases. A similar look-up table also preferably is used for the dry, cement delivery system to determine the step rate of the dry cement. In an alternative embodiment, another look-up table may be provided that correlates the delivery characteristics of the hopper for a given speed (or position) of the valve 45. Thus, by accessing this look-up table, the system controller 100 can approximately determine the quantity of dry cement that will be delivered if the valve operates at a given speed or is set at a particular position. This feature is especially useful if an automatic start-up is desired.

The system controller 100 preferably connects electrically to: (a) the input flow meter 37; (b) the star wheel speed sensor 47; (c) the sonic level sensor 65; (d) the density meter 95; and (e) the discharge flow meter 87, for receiving electrical output signals from each of these sensors. These signals from each of the sensors are processed as described more fully below to permit automatic operation of the ACS.

The system controller 100 also preferably connects electrically to: (a) the fresh water device 35; and (b) the valve controller 46, for providing output control signals to each of these components. The controller automatically adjusts the speed or position of the fresh water device 35 and the valve 45 to fine-tune the density of the slurry, as will be described more fully below.

I. OPERATION OF SYSTEM CONTROLLER

Referring now to FIGS. 2A-2F, the operation of the system controller 100 will be discussed in accordance with the preferred embodiment. In the preferred embodiment, the system controller provides a menu display to the operator to guide the operator through both the main menu and through each step of the options. As shown in FIG. 2, the system controller initially provides three options, as part of a main menu, to the operator: (1) enter job data into the ACS (Job Entry Data); (2) calibrate and set-up the ACS (Cal & Setup); or (3) run the ACS (Run). The source code for the preferred programming of the controller is attached in the Appendix, incorporated by reference.

1. Entering Job Data

If the operator selects the Job Entry Data selection on the main menu, the controller will ask in step 202 whether the operator wishes to clear all stage data, or whether the operator wishes to edit existing data. It should be understood that the operation of the ACS could include a number of stages, with a stage being defined as any change in operating conditions, including a change in the cement slurry's target density, a change in the density of the input fluid, or a change in the density or type of dry cement that is used. Thus, for example, if it is desired to change from a target slurry of 16.0 PPG to 16.3 PPG, a different stage would be involved. Similarly, if it was desired to add liquid additives to the input water after operations had begun, thus changing the density of the input liquid, a different stage would be defined. Changing from one stage to the next could be preprogrammed into the system controller by, for example, specifying the volume (either input or discharge) at which the stage was to change, or could be done manually by having the operator designate a change in stage by activating a switch. In either instance, the stage parameters could be preprogrammed into the controller.

The first display that will appear to the operator after the stages are cleared, or if the edit option is chosen, is a request, in step 204, to input the desired or target density, preferably in pounds per gallon (PPG), for the cement slurry for that particular stage. As one skilled in the art will realize, other measurement units may be used without departing from the principles of this invention. In the preferred embodiment, an increment and decrement switch is used to set the desired setting. Obviously, other input procedures could be used without departing from the scope of the present invention. After the target density for the cement slurry is entered for a particular stage, the controller prompts the operator in step 206 to enter the specific gravity of the input fluid for that particular stage, again through the use of the increment and decrement switches. The controller next requests information regarding the dry cement specific gravity for that particular stage in step 208.

Once these three items are entered by the operator, the controller in step 210 asks the operator if there are other stages to be entered at this time. If there are, then the controller cycles back through the menus to obtain the necessary information. When all stages have been entered, the controller permits the operator to review the information entered, by stage, and make any necessary changes. When review is complete, the controller returns to the main menu which again is displayed to the operator.

2. Calibrating and Setting Up the System

If the operator selects the Calibrate and Setup option, then the controller will first ask the operator in step 215 if he or she wishes to change the operating parameters or to calibrate the input mix water flow meter. For example, if the input flow meter 37 provides output pulses to signify to the controller 100 that 10 gallons/minute have flowed through the meter, the operator could recalibrate the controller to interpret the 100 pulses from the input flow meter to mean that 10.5 gallons/minute have flowed through the meter. The operator, therefore, can adjust the k factor of the input meter. Similarly, in step 217, the operator also can change the k factor of the discharge meter. This feature enables the various sensors to be pretested and finely tuned for accuracy. In addition, if a new meter is substituted, the meter can be quickly and accurately calibrated through the use of this software option.

In step 219, the controller asks the operator if he or she wishes to change the settings of the valve on the dry cement source. Three different parameters can be changed on the valve. The first parameter that can be changed is the response factor during normal run operations. The response factor represents the gain or amount of change that is used when the dry cement rate must be changed. If a discrepancy exists between the actual and desired rate of which dry cement is supplied, the actual race must be changed by a certain amount. If the amount of change is excessive and the system is over-correcting, oscillation could occur. Consequently, a gain correction is used which is only a percentage of the difference between desired and actual rates. The second parameter that can be altered is the k factor that represents the interaction between the controller and the k factor permits calibration of the sensor. Lastly, the start-up gain of the valve can be adjusted. The start-up gain is the response factor of the valve during start-up operations, which is similar to the response factor during normal operation. All of these factors can be adjusted to fine tune the operation of the dry cement valve.

The controller also asks the operator if it is necessary to adjust the density meter in step 221. The operator can adjust the controller so that the maximum output from the density meter represents a specific density value. Similarly, the operator can recalibrate the controller so that the lowest output from the density meter represents a zero density value. Thus, for example, if the density meter provides an output that ranges between 0.01 to 0.20 amperes, the controller would correlate the 0.01 amps to a zero density, and would correlate the 0.20 amps to the maximum density value, which might be, for example, 20.0 PPG.

Finally, the controller asks the operator if the mix water response should be readjusted in step 223. The mix water response, like the response factor of the dry cement rate, regulates the gain by which the mix water is adjusted, to prevent over-correction.

3. Run Mode

If the operator selects the Run option off of the Main Menu, the system begins automatic operation. In the preferred embodiment, the Run mode is selected after initialization and startup of the system.

In step 301, the controller calculates the current stare and running parameters, and then displays a screen (not shown) for the operator. The display screen preferably includes mix water rate, discharge rate, target density, actual density measured by the density meter 95, the stage, the total discharge, the stage discharge, and the time.

After the screen is displayed (or updated), the Controller 100 determines in step 303 if the operator has requested that the system proceed to the next stage. This preferably is done by depressing a preselected switch for a predetermined minimum time. Alternatively, the stage may be changed by a key board entry, or automatically is a predetermined volume of slurry has been discharged.

In step 305, the Controller 100 determines whether the PPG trim feature has been activated and, if activated, determines the amount of trim selected. Next, in step 307, the Controller reads the tub level measured by tub level sensor 65 and scales that measurement to a physical unit (such as feet or inches) for future reference. Similarly, in step 309, the controller reads the density measured by density meter 95 and scales that measurement to a physical unit (such as pounds per gallon or PPG).

In step 310, the controller determines if the automatic density correction feature has been enabled by the operator. In the preferred embodiment, a switch is provided that permits the operator to automatically correct the density through the use of the density meter 95 as a feedback device. In normal operation, the controller maintains the level in slurry in Chamber B constant, and then determines the amount of mix water and dry cement that is being discharged as slurry. These numbers are used to automatically regulate the rate of mix water and dry cement being input to the mixing chamber. In addition to this normal operation, the ACS also has the capability to monitor the actual density of the slurry by means of the density meter 95. According to the preferred embodiment, the operator must select this feature.

If the automatic density correction feature is selected, the controller, as shown in step 311, determines if the actual density measured by the density meter 95 is above or below the target density. If the actual density is higher than the target density, the target density is automatically decreased, which will result in the actual density being decreased as ratios of mix water and dry cement are changed.

Conversely, if the measured density is low, the target density is automatically increased, thus causing the actual density to increase as the ratio of mix water and dry cement change. According to the preferred embodiment, the target density is only increased or decreased each cycle by five percent (5%) of the difference between actual density and target density. This is done to prevent overcompensation and wide fluctuations.

If the automatic density correction is not selected, or if after it is complete, the controller in step 312 determines what the actual mix water rate is into the mixing chamber. To determine the mix water rate, the controller proceeds to the low level interrupt shown in FIG. 5 to gather the period for measurement and the amount of flow. FIG. 5 is a subroutine that measures pulses off of the input flow meter 37 and generates a period and a total. The controller, in step 312 uses the total number of pulses for the period, and determines the amount of flow by referring to the k factor obtained during calibration and set-up for the mix water flow meter. Once the amount of flow and period are ascertained by the controller, the flow is divided by the period to obtain the mix water rate.

In similar fashion in step 313, the controller determines the discharge rate. The controller proceeds to the low level interrupt shown in FIG. 6. FIG. 6 is a subroutine that measures pulses off of the discharge flow meter 87 and generates a period and a total flow. The controller uses the total number of pulses generated by the discharge flow meter for that period, together with the k factor obtained during calibration and set-up for the discharge flow meter, to determine the amount of slurry discharged during the period. The controller then divides the amount of slurry discharged, by the period, to determine the discharge rate.

In step 315, the controller checks to determine if the discharge rate has changed by more than one-half of a barrel in a second. If such a change is detected, the controller reverts to the start-up mode. Next, in step 317, the controller determines if the discharge rate has passed below a minimum threshold. If this occurs, the ACS is shut down.

In step 319, the controller determines the percentage of volume of cement slurry that should be mix water, and then calculates the proper mix water rate. According to the preferred embodiment, the controller determines the percentage of mix water (or fluid) by volume in the cement slurry. This is done by first determining the percentage of dry cement by volume of slurry as follows:

% VOLUME OF CEMENT=(SLURRY SG-FLUID SG)/(CEMENT SG-FLUID SG), (1)

wherein

SLURRY SG represents the target or desired density of slurry in specific gravity units. This means the target density, which according to the preferred embodiment is entered in pound per gallon (PPG) by the operator in step 204, must be convened by controller into specific gravity units;

FLUID SG represents the density of the input fluid in specific gravity units, as entered by the operator in step 206. Where water is used as the input fluid, this number is 1.0; and

CEMENT SG represents the absolute density of the dry cement in specific gravity units, as entered by the operator in step 208.

Once the percentage volume of cement (% VOLUME OF CEMENT) is calculated, the percentage volume of liquid may be easily calculated, as follows:

% VOLUME OF LIQUID=1.00-% VOLUME OF CEMENT.                (2)

After the controller determines the % VOLUME OF LIQUID, the controller multiplies this number by the DISCHARGE FLOW RATE to determine the optimal rate at which the input fluid (or mix water) should be supplied to the mixing chamber.

In step 321, after the optimal mix water rate is determined in step 320, this optimal rate is compared with the mix water rate measured in step 312 to determine if the measured mix water rate is less than the optimal rate. If the measured rate is less than the optimal or desired rate, the controller determines if the ACS is in a start-up mode in step 322. Depending on whether the ACS is in a start-up mode, the controller accesses one of two look-up tables--one for start-up mode and one for normal operation. Each of the look-up tables defines a step rate associated with the particular magnitude of error between the measured mix water rate and the desired or optimal mix water rate. Each magnitude of error is associated with a particular step rate in the look-up table. The step rate represents how quickly the mix water rate will be increased or decreased.

For example, if the controller determines in step 321 that the measured mix water rate is 5 gallons per minute less than the optimal rate, the controller, in step 323 or 324 (depending on whether the ACS is in normal operation or start-up), will access a look-up table, determine what step rate is associated with a discrepancy or error of 5 gallons per minute. If the error or discrepancy is very small, the step rate may be zero to reflect no change and to prevent overcompensation. In the preferred embodiment, the look-up is preprogrammed into read only memory ("ROM").

After the controller determines the appropriate step rate is either step 323 or 324, a direction flag is activated to remind the controller that the actual mix water rate must be increased. Conversely, in steps 325, 326, and 327, if the mix water rate is too high, the controller determines the magnitude of the error or discrepancy between measured mix water rate and optimal mix water rate, and determines from the appropriate look-up table what the proper step rate is. After the step rate is determined, the direction flag is activated down to remind the controller that the actual mix water rate must be decreased by the step factor.

Because a separate look-up table is used for the start-up mode and for normal operation, the reaction of the system can be fine-tuned to permit quicker (or slower) response for start-up than would be desired for normal operation. After the appropriate step rate and directional information has been found, it can be stored in step 329. In the preferred embodiment, the information is stored by means of pulse width modulation.

The stored step rate and directional information for mix water rate is retained by the interrupt task shown in FIG. 4. In the preferred embodiment, the interrupt of FIG. 4 occurs at a 0.040 second rate. The mix water interrupt determines in step 251 the step rate and directional information. In response, the controller increases or decreases the speed or position of the input water device 35 in accordance with the step rate and directional information.

In step 335, the controller obtains the rate at which dry cement is supplied by dry cement source 40. A sensor 47 on the dry cement source 40 generates pulses that are retrieved in the low level interrupt of FIG. 7. The controller converts the pulses into rate information by means of the k factor.

After determining the rate at which dry cement is being introduced into the mixing chamber, the controller determines in step 337 if the system is in the start-up mode and branches accordingly. Regardless of whether the system is in start-up, the controller performs a number of calculations in steps 338, 339 to determine the amount of bulk cement required.

The first calculation performed in steps 338, 339 is to determine the WEIGHT PER CUBIC FOOT OF MIX WATER (or "HO") as follows:

HO=7.4805*8.3452984*WATER SG                               (3)

7.4805 represents gallons per cubic foot;

8.3452984 represents pounds per gallon; and

WATER SG is the density of the mix water or input fluid in specific gravity units, as entered by the operator in step 206.

Next, the controller calculates the % of "REAL" DRY CEMENT ("CO") in the total bulk volume of the dry cement, as compared to the percentage of air in the total bulk volume of dry cement, as follows:

CO=BULK WEIGHT OF DRY CEMENT/(CEMENT SG*HO),               (4)

Where,

BULK WEIGHT OF DRY CEMENT is the weight of dry cement in a sack of cement;

CEMENT SG represents the absolute density of the dry cement in specific gravity units; and

HO is the weight per cubic feet of mix water found in calculation (3).

The controller then determines the ABSOLUTE VOLUME OF DRY GALLONS PER MINUTE ("DRY GALLONS MINUTE"), as follows:

DRY GALLONS MINUTE=CUBIC FEET MINUTE DRY*7.4805            (5)

Where

CUBIC FEET MINUTE DRY represents the quantity of cubic feet of dry cement added each minute.

Finally, the controller determines the desired rate of dry cement ("DRY DEMAND") to be supplied as follows:

DRY DEMAND=DISCHARGE FLOW RATE*% VOLUME OF CEMENT          (6)

Where

DISCHARGE FLOW RATE is the measured discharge flow rate found in step 313; and

% VOLUME OF CEMENT is the percentage of dry cement by volume of slurry, as calculated in step 319.

If the controller determines in step 337 that the ACS was in a start-up mode, the controller branches to path 341. After calculating the rate of dry cement required in step 338, the controller compares this rate with the actual rate determined in step 335. If the controller determines in step 344 that the actual rate at which dry cement is being delivered is lower (or higher) than the desired rate, then the controller branches to step 346 (or step 348) where a step rate is obtained and a directional flag is set. The step rate preferably is found in a look-up table, associated with a particular magnitude of error. Thus, the controller determines the error or discrepancy between the actual dry cement rate and the desired rate, and looks up that error in the look-up table to find the step rate that should be used to correct the actual rate at which dry cement is delivered.

After the step rate is found, the current tub level is stored in memory in step 350. If, conversely, the ACS is not in a start-up mode, then the controller follows branch 342. After determining the desired rate of dry cement to be supplied, the controller in step 360 determines the level in Chamber B. In step 362, the controller compares the level measured in Chamber B with the level stored in memory during start-up (step 350). If a difference exists in tub level, the controller determines the magnitude of the difference in step 363 or 364, and then multiplies the difference by the dry demand found in step 339 to obtain a "tub factor". The tub factor then is either added to or subtracted from the dry demand calculated in step 339 to obtain a modified dry demand that then is used.

Next, in step 370, the controller compares the desired modified rate at which dry cement should be delivered with the actual rate. In steps 371 and 372 the controller determines the appropriate step rate from the look-up table. After the appropriate step rate has been found, the controller in step 375 shows the step rate and directional information, preferably in a pulse width modulated signal. This signal is retrieved in the Dry Feed Interrupt of FIG. 3. As shown in FIG. 3, the speed or position of the dry cement valve is altered according to the step rate and directional rate obtained from step 371 (or step 372). In step 380, the controller determines if the tub is maintaining a constant level and sets the appropriate flags.

II. ACS OPERATION

The operation of the ACS system will now be described with reference to FIG. 1. The operation of the ACS preferably comprises an initialization mode, a start-up mode, a run mode, a trim mode, and a rate variance mode.

A. Cementing Initialization

To initiate the ACS, the operator manually (1) opens the input water valve 36 to permit water to flow into the mixing chamber 60; and (2) adjusts the speed of the rotary valve 45 to regulate the delivery of dry cement into the mixing chamber 60. Because the discharge valve 85 has yet to be opened, the slurry will be forced to recirculate through recirculation line 90. As the slurry flows through recirculation line 90, the density meter 95 measures the density of the slurry. Alternatively, the density can be measured manually by an operator.

Recirculation continues in this manner until two conditions occur: (1) the density measured is the same as the target or desired density, and (2) the level of cement in Chamber B of mixing Chamber 60 lies between the levels marked in FIG. 1 as xo and x1. At any time prior to starting the run mode, the operator enters into the system controller 100 the following information for each operating stage: (a) the desired or target slurry density; (b) the density of the water or other base liquid being supplied through input line 30; and (c) the density of the dry cement being used.

B. ACS Startup

After the ACS system has been initialized, the operator opens the discharge valve 85 to allow the cement slurry to be discharged through discharge line 80. At this time, the ACS controller 100 receives an output signal from the discharge flow meter 87 indicating that discharge flow has begun. The operator also manually sets the discharge pumps 89 located downstream in the slurry discharge line 80 to operating speed. When the discharge pumps 89 are brought up to operating speed, the level of slurry in Chamber B begins to fall.

Simultaneously, ACS controller 100 regulates the input water rate by adjusting the fresh water positive displacement pump 35 to maintain a constant high precision ratio of input water rate to discharge cement rate. This is done by receiving a signal that represents the rate of flow of cement slurry through the discharge flow meter 87 and by determining the percentage of water by volume in the cement slurry. The controller 100 multiplies the discharge flow rate by the percent of water by volume to determine the amount and rate of water that is being discharged. Once this flow rate of water is determined, the controller 100 adjusts the fresh water pump to this rate. Thus, the controller 100 precisely controls the rate at which water is injected into the mixing chamber 60 so that it is the same as the amount of water that is discharged from the mixing chamber 60 (as part of the slurry). As a result, it is possible to obtain very precise control of the density of the slurry.

According to the preferred embodiment, the controller 100 determines the percentage of water (or liquid) by volume in the cement slurry by first determining the percentage of dry cement by volume in the slurry. The percentage of cement by volume of slurry is calculated as follows:

% VOLUME OF CEMENT=(SLURRY SG-FLUID SG)/(CEMENT SG-FLUID SG),

wherein

SLURRY SG represents the target or desired density of slurry in specific gravity units. This means the target density, which according to the preferred embodiment, is entered in pound per gallon (PPG) by the operator in step 204, must be converted by controller into specific gravity units;

FLUID SG represents the density of the input fluid in specific gravity units, as entered by the operator in step 206. Where water is used as the input fluid, this number is 1.0; and

CEMENT SG represents the absolute density of the dry cement in specific gravity units, as entered by the operator in step 208.

Once the percentage volume of cement (% VOLUME OF CEMENT) is calculated, the percentage volume of liquid may be easily calculated, as follows:

% VOLUME OF LIQUID=1.00-% VOLUME OF CEMENT.

This equation assumes that only two ingredients are combined to form the slurry--input liquid and dry cement. Additives may be provided as long as they are added to either the dry cement or to the input liquid prior to their introduction to the system.

After the controller 100 calculates the % VOLUME OF LIQUID, the controller 100 multiplies this number by the DISCHARGE FLOW RATE to determine the rate at which the input fluid should be supplied to the mixing chamber 60. The controller then sets the input pump at the proper speed to supply the input liquid at the requisite rate. The controller monitors the output from the input flow meter 37 to adjust the input pump 35 to the proper setting.

For example, if the discharge flow meter indicates that slurry is being discharged at 420 gallons/minute, and the controller determines from the operator inputs that the % VOLUME OF CEMENT is 0.519, then the controller determines that the % VOLUME OF FLUID is 0.481. The controller 100 multiplies the % VOLUME OF LIQUID by the DISCHARGE FLOW RATE, as follows: 0.481×420 gallons/minutes=202 gallons/minute of input liquid. The controller 100 then sets the speed of the fresh water pump 35 at a speed to inject 202 gallons/minute. The input flow meter 37 provides feedback to the controller 100 of the actual rate of liquid being injected into the mixing chamber 60 to permit the controller to readjust the speed of the fresh water pump 35 to precisely control the rate at which liquid is supplied to the mixing chamber 60.

At approximately the same time that the ACS controller 100 is setting the speed of the fresh water pump 35, it also is adjusting the speed of the valve 45. The ACS controller 100, as noted, determines the amount of liquid that must be injected into the mixing chamber 60 to obtain the desired slurry density at the fixed discharge rate. At the same time, the ACS controller 100 also calculates the rate at which the dry cement must be delivered from the source 40 to achieve the desired slurry density.

C. ACS Run Mode

Ideally, if the input flow meter 37 is extremely accurate permitting precise control of the fresh water pump 35, and if the discharge flow meter 87 is equally accurate, and if the valve 45 is delivering cement at the proper rate, so that the amount of dry cement and water being supplied to the mixing chamber 60 exactly equals the amount of cement and water being discharged as slurry, then the level of cement slurry in Chamber B will be fixed and stable, and the actual density of the discharged slurry will equal the desired slurry density input by the operator into the ACS controller 100. In other words, if all meters and valves are completely accurate, the level of slurry in Chamber B will be constant at this time.

If, conversely, the level of cement slurry changes or fluctuates in Chamber B, then the controller assumes there has been a fluctuation in bulk density of the dry cement and modifies its bulk density calculation. The controller then determines how much to change the delivery rate of the dry cement to maintain tub level and proper slurry density. This is explained more fully in the flow chart shown in FIG. 2, and described above. Once the proper rate of dry cement is determined, the position or speed of valve 45 is changed as required.

D. PPG Trim

After the actual and desired slurry density readings are equal, it is common to take a sample of the cement slurry being discharged to test it. Alternatively, another density sensor may be provided downstream in the slurry discharge line. If the density of the sample discharge (or of the second density sensor) does not correspond to the density measured by density meter 95, then the operator can elect to use the ACS PPG Trim mode by pressing an appropriate switch on the control panel (not shown). Activation of this trim switch will be transmitted to the ACS system controller 100, which, in response will cause the ACS to operate in the trim mode. The trim switch permits the operator to manually alter the mix water/dry cement ratio in response to discrepancies between the target density and measured density.

In the trim mode, the controller 100 adjusts the ratio of input water rate to discharge cement slurry rate, which was based upon the percent of water by volume obtained from the calculations relating to the cement slurry discharge. By changing this ratio, the rate at which water is to be supplied to the mixing chamber 60 also will change, as will the rate at which dry cement is delivered to the mixing chamber 60. As a result, the operation of the ACS will revert to the Startup Mode after the ratio of input water rate to discharge slurry rate is changed, and the controller 100 will proceed to determine the proper operating speed or position of the input device 35, based upon the new ratio. After the speed or position of input device 35 is set, then the speed of valve 45 is set to an approximate value based upon desired demand of dry cement. The controller 100 then monitors the output from the level sensor 65 and adjusts the desired dry demand rate until the slurry level in Chamber B remains constant.

E. Discharge Rate Variance

If during ACS operation, the discharge rate changes from its fixed value for any reason, then ACS returns to the Start-up Mode. After detecting a large change in the discharge rate, the controller returns to the start-up mode, where a mix water rate is calculated. The controller 100 sets the input device 35 to the necessary setting so that the amount of water entering through input line 30 equals the amount of water leaving as slurry through the discharge line 80. The input flow meter 37 is used by the controller 100 as part of a closed loop feedback system to precisely set the rate of the device 35. After the mix water input rate is set, the controller then determines the approximate speed of valve 45 that will provide the same amount of dry cement as is leaving as a component of the slurry. The controller 100 monitors the level sensor 65 and adjusts the dry cement rate as necessary to maintain the level of slurry in Chamber B constant.

Operation of the ACS system preferably continues until the total volume of slurry discharged equals the total volume entered by the operator into controller 100 at the beginning of the operation or until the operator indicates that it is time to begin a new stage. The controller 100 keeps track of total volume based upon the signals from the discharge flow meter 87. The controller 100 preferably obtains a signal from the discharge flow meter 87 once every 1/x of a second. Thus, the controller multiplies each rate signal from the discharge flow meter 87 and multiplies that rate by 1/x to obtain a number that represents the total volume of slurry that has been discharged during that sampling period. The controller keeps a running count of the discharged volume by adding each new volume to the total accumulated volume, and compares the new total with the desired total. When the accumulated total equals or is greater than the desired volume, the controller 100 terminates operation and notifies the operator that the job is complete.

While a preferred embodiment of the invention has been disclosed, various modifications can be made to the preferred embodiment without departing from the principles of the present invention.

Claims (24)

We claim:
1. An automatic cementing system, comprising:
a mixing chamber with a first chamber for receiving liquid and dry cement and a second, relatively deeper chamber to which the first chamber discharges, said chambers mixing the liquid and dry cement together to form a cement slurry;
an input line for supplying the liquid to said first chamber;
means for supplying the dry cement to said first chamber, said supplying means including a means for regulating the rate at which dry cement is delivered;
a level sensor located in said second chamber for measuring a change in level in said second chamber;
a discharge line connected to said second chamber for supplying the cement slurry; and
a system controller electrically connected to the regulating means on said supplying means, and to the level sensor, for receiving signals at very short predetermined intervals from said level sensor indicating a change in slurry level in said second chamber and controlling said regulating means to maintain the level of slurry in the second chamber substantially constant.
2. A system as in claim 1, further comprising;
an input device on said input line for controlling the rate at which liquid is added to the mixing chamber;
a discharge flow meter on said discharge line electrically connected to the system controller:
said system controller receiving a signal from the discharge flow meter indicating the flow rate of cement slurry and regulating the input device to add liquid to the mixing chamber at the same rate as the liquid is discharged in the slurry.
3. A system as in claim 2, wherein said input device is a positive displacement pump.
4. A system as in claim 2, wherein the system controller receives a signal from said discharge flow meter and in response regulates the operation of said input device.
5. A system as in claim 4, wherein the system controller receives data inputs from an operator, calculates the percentage of liquid in the cement slurry based upon the data inputs and controls the operation of the input device to maintain the ratio of the rate of the liquid delivered to the mixing chamber to the rate of the slurry discharged from the second chamber substantially constant.
6. A system as in claim 5, wherein the discharge flow meter has an accuracy of approximately 0.5 percent or better.
7. A system as in claim 6, wherein the discharge flow meter is a non-intrusive flow meter.
8. An automated system for controlling the density of a cement slurry, comprising:
a mixing chamber with a first chamber for receiving dry cement and water to produce a cement slurry, and a second chamber for receiving overflow from the first chamber;
a level sensor in said second chamber for detecting a change in slurry level in said second chamber and for providing an output signal indicative of a change in slurry level;
an input line, including an input device, for supplying liquid to the mixing chamber at a particular rate;
a means for delivering dry cement to said mixing chamber, wherein the delivery of dry cement from said delivery means is controlled by a valve;
a system controller for receiving the output signal from said level sensor and for providing a control signal to said valve to modify the delivery of the dry cement so as to maintain the level of cement slurry substantially constant in said second chamber.
9. A system as in claim 8, further including;
a discharge line connected to said second chamber for discharging the cement slurry from said second chamber, said discharge line including a discharge flow meter providing an output signal to said system controller that is indicative of the rate of slurry being discharged;
wherein the setting of the input device and the valve is dependent upon the output signal from said discharge flow meter.
10. A system as in claim 9, further comprising:
a density meter in the discharge line in electrical connection with the system controller for providing a signal representative of the slurry density:
wherein the system controller corrects the setting of the input device and the valve as a function of the signal from the density meter.
11. An automatic cementing system, comprising:
a mixing chamber for receiving mix water and dry cement, and for mixing the liquid and dry cement together to form a cement slurry;
an input line with an input device for supplying the mix water at a particular rate;
means for delivering the dry cement, which includes a regulating means for controlling the rate at which the dry cement is delivered;
a discharge line with a discharge pump and a discharge flow meter for measuring the rate at which slurry is discharged from the mixing chamber and for providing an output signal indicative of said rate;
a system controller electrically connected to the input device, the regulating means and the discharge flow meter, for receiving a discharge flow rate signal from the discharge flow meter and for providing control signals to the input device;
wherein the system controller provides a control signal to the input device to control the rate at which mix water is supplied to the mixing chamber based upon the discharge flow rate signal;
wherein the system controller determines the percentage of mix water in the cement slurry and the amount of mix water being discharged in the cement slurry from the mixing chamber, and modifies the input device to provide an equal amount of mix water into the mixing chamber.
12. A system, as in claim 11, wherein the system controller also sets the regulating means based upon the discharge flow rate signal.
13. A system as in claim 12, wherein the system controller determines the percentage of dry cement in the cement slurry and the amount of dry cement being discharged in the cement slurry, and modifies the regulating means to provide an equal amount of dry cement into the mixing chamber.
14. A system as in claim 13, wherein the regulating means comprises a rotary valve with an internal control unit.
15. A system as in claim 14, further comprising a speed sensor for providing feedback to the system controller recording the actual speed of the rotary valve.
16. A system, as in claim 11, further comprising;
an input flow meter for providing feedback to the controller indicative of input flow rate to enable the controller to precisely set the input device.
17. A system as in claim 11, wherein the delivering means comprises a dry cement hopper, and the dry cement hopper includes;
a weight sensor for determining the weight in the hopper; and
a cement inlet control valve for regulating the amount of dry cement that is blown into the hopper.
18. A system as in claim 11, further comprising;
a level sensor in the mixing chamber for monitoring a change in the level of slurry in the mixing chamber, said level sensor electrically connected to said system controller for providing an indication of a change in level to the controller, and said controller adjusting the speed of the regulating means in response to the indication of a change in level.
19. A system as in claim 18, wherein the mixing chamber comprises a first chamber for receiving liquid and slurry, and a second chamber to receive any overflow from the first chamber, with the discharge line connected to the second chamber and the level sensor being located in the second chamber.
20. A system as in claim 19, wherein the second chamber is relatively deep, but has a relatively small cross-section to enable the level sensor to easily detect changes in slurry level in the second chamber.
21. A system as in claim 11, further comprising;
a recirculation line connected to said discharge line for recirculating slurry to the mixing chamber.
22. A system as in claim 11, further comprising;
a density meter for measuring the density of the slurry and providing an electrical signal to the system controller indicative of the measured density.
23. A system as in claim 22, wherein the controller compares the density measured by said density meter with a preprogrammed desired density, and generates a correction factor if a discrepancy exists.
24. A system as in claim 23, wherein the controller adjusts the rate of the input device based upon the correction factor.
US08470976 1989-08-02 1995-06-06 Automatic cementing system for precisely obtaining a desired cement density Expired - Lifetime US5590958A (en)

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US08178659 US5503473A (en) 1989-08-02 1994-01-07 Automatic cementing system for precisely obtaining a desired cement density
US08470976 US5590958A (en) 1989-08-02 1995-06-06 Automatic cementing system for precisely obtaining a desired cement density

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Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000037770A1 (en) * 1998-12-21 2000-06-29 Baker Hughes Incorporated Closed loop chemical injection and monitoring system for oilfield operations
US6085912A (en) * 1999-07-13 2000-07-11 Hacking, Jr.; Earl L. Apparatus for sorting and recombining minerals background of the invention
US20050155763A1 (en) * 2004-01-16 2005-07-21 Reddy B. R. Settable fluids comprising particle-size distribution-adjusting agents and methods of use
US20050161107A1 (en) * 2004-01-23 2005-07-28 Mark Turnbull Apparatus and method for loading concrete components in a mixing truck
US20050166961A1 (en) * 1998-12-21 2005-08-04 Baker Hughes Incorporated Closed loop additive injection and monitoring system for oilfield operations
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US20060233039A1 (en) * 2005-04-14 2006-10-19 Halliburton Energy Services, Inc. Control system design for a mixing system with multiple inputs
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US20060272819A1 (en) * 2004-01-16 2006-12-07 Halliburton Energy Services, Inc. Methods of preparing settable fluids comprising particle-size distribution-adjusting agents, and associated methods
US20080053221A1 (en) * 2006-09-06 2008-03-06 Allen Thomas E Method for determining absolute density of cement slurry
US20090294123A1 (en) * 2008-06-03 2009-12-03 Baker Hughes Incorporated Multi-point injection system for oilfield operations
US20100172202A1 (en) * 2009-01-08 2010-07-08 Halliburton Energy Services, Inc. Mixer system controlled based on density inferred from sensed mixing tub weight
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US20100329797A1 (en) * 2008-12-17 2010-12-30 James M. Duncan Modified Storage Pod and Feeding System for Binder Utilized for In-Situ Pilings and Method of Utilizing the Same
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Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JPH0967830A (en) * 1995-08-31 1997-03-11 Komatsu Ltd Controlling device for soil improvement machine
US5795060A (en) * 1996-05-17 1998-08-18 Stephens; Patrick J. Method and apparatus for continuous production of colloidally-mixed cement slurries and foamed cement grouts
EP0924040A1 (en) * 1997-12-17 1999-06-23 Esi Elettrosistemi S.r.l. A device for gauging the consistency of a mixture during mixing in a rotary recipient
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US7561943B2 (en) * 2005-12-30 2009-07-14 Halliburton Energy Services, Inc. Methods for volumetrically controlling a mixing apparatus
US20070153624A1 (en) * 2005-12-30 2007-07-05 Dykstra Jason D Systems for determining a volumetric ratio of a material to the total materials in a mixing vessel
US7567856B2 (en) * 2005-12-30 2009-07-28 Halliburton Energy Services, Inc. Methods for determining a volumetric ratio of a material to the total materials in a mixing vessel
US20070171765A1 (en) * 2005-12-30 2007-07-26 Dykstra Jason D Systems for volumetrically controlling a mixing apparatus
US9010989B2 (en) 2008-04-14 2015-04-21 Schlumberger Technology Corporation Container system
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US20170259457A1 (en) * 2016-03-14 2017-09-14 Schlumberger Technology Corporation Mixing System for Cement and Fluids

Citations (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2658644A (en) * 1947-12-10 1953-11-10 Proportioneers Inc Apparatus for proportioning materials
US3004544A (en) * 1955-12-29 1961-10-17 Texaco Inc Continuously measuring slurry density
US3161203A (en) * 1961-07-06 1964-12-15 Halliburton Co Method and apparatus for precision blending of composite fluid mediums
US3326536A (en) * 1962-05-09 1967-06-20 Dow Chemical Co Mixing apparatus
US3379421A (en) * 1966-12-14 1968-04-23 Westinghouse Electric Corp Control of material processing device
US3757864A (en) * 1971-05-12 1973-09-11 Dow Chemical Co Friction reducing and gelling agent for organic liquids
US3818991A (en) * 1971-05-20 1974-06-25 Dow Chemical Co Method of treating subterranean formation with a composition of improved viscosity control
US3980136A (en) * 1974-04-05 1976-09-14 Big Three Industries, Inc. Fracturing well formations using foam
US4003431A (en) * 1972-09-20 1977-01-18 Byron Jackson, Inc. Process of cementing wells
US4091462A (en) * 1975-09-23 1978-05-23 Toto Electric Industry Co. Control apparatus for mortar compounding apparatus
US4126181A (en) * 1977-06-20 1978-11-21 Palmer Engineering Company Ltd. Method and apparatus for formation fracturing with foam having greater proppant concentration
US4176064A (en) * 1977-06-20 1979-11-27 Palmer Engineering Company Ltd. Mixture concentrator
US4209258A (en) * 1978-02-14 1980-06-24 Oakes W Peter Automatic continuous mixer apparatus
US4265266A (en) * 1980-01-23 1981-05-05 Halliburton Company Controlled additive metering system
US4265262A (en) * 1979-03-19 1981-05-05 William Hotine Fluent material level control system
US4298288A (en) * 1980-01-25 1981-11-03 Anthony Industries, Inc. Mobile concreting apparatus and method
US4327759A (en) * 1979-08-24 1982-05-04 Wimpey Laboratories Limited Slurry producing apparatus
US4353482A (en) * 1980-01-23 1982-10-12 Halliburton Company Additive metering control system
US4436431A (en) * 1981-05-11 1984-03-13 William A. Strong Slurry production system
US4456069A (en) * 1982-07-14 1984-06-26 Vigneri Ronald J Process and apparatus for treating hydrocarbon-bearing well formations
US4474204A (en) * 1983-07-22 1984-10-02 The Western Company Of North America Delivery and metering device control system
US4475818A (en) * 1983-08-25 1984-10-09 Bialkowski Wojciech L Asphalt coating mix automatic limestone control
US4538222A (en) * 1983-04-06 1985-08-27 Halliburton Company Apparatus and method for mixing a plurality of substances
US4665982A (en) * 1986-06-26 1987-05-19 Brown Billy R Formation fracturing technique using liquid proppant carrier followed by foam
US4701095A (en) * 1984-12-28 1987-10-20 Halliburton Company Transportable material conveying apparatus
US4726219A (en) * 1986-02-13 1988-02-23 Atlantic Richfield Company Method and system for determining fluid pressures in wellbores and tubular conduits
US4779186A (en) * 1986-12-24 1988-10-18 Halliburton Company Automatic density control system for blending operation
US4845981A (en) * 1988-09-13 1989-07-11 Atlantic Richfield Company System for monitoring fluids during well stimulation processes
US4887670A (en) * 1989-04-05 1989-12-19 Halliburton Company Controlling fracture growth
US4911241A (en) * 1989-01-27 1990-03-27 Dowell Schlumberger Incorporated Constant viscosity foam
US4930576A (en) * 1989-04-18 1990-06-05 Halliburton Company Slurry mixing apparatus
US5114239A (en) * 1989-09-21 1992-05-19 Halliburton Company Mixing apparatus and method
US5281023A (en) * 1989-08-02 1994-01-25 Stewart & Stevenson Services, Inc. Method and apparatus for automatically controlling a well fracturing operation

Patent Citations (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2658644A (en) * 1947-12-10 1953-11-10 Proportioneers Inc Apparatus for proportioning materials
US3004544A (en) * 1955-12-29 1961-10-17 Texaco Inc Continuously measuring slurry density
US3161203A (en) * 1961-07-06 1964-12-15 Halliburton Co Method and apparatus for precision blending of composite fluid mediums
US3326536A (en) * 1962-05-09 1967-06-20 Dow Chemical Co Mixing apparatus
US3379421A (en) * 1966-12-14 1968-04-23 Westinghouse Electric Corp Control of material processing device
US3757864A (en) * 1971-05-12 1973-09-11 Dow Chemical Co Friction reducing and gelling agent for organic liquids
US3818991A (en) * 1971-05-20 1974-06-25 Dow Chemical Co Method of treating subterranean formation with a composition of improved viscosity control
US4003431A (en) * 1972-09-20 1977-01-18 Byron Jackson, Inc. Process of cementing wells
US3980136A (en) * 1974-04-05 1976-09-14 Big Three Industries, Inc. Fracturing well formations using foam
US4091462A (en) * 1975-09-23 1978-05-23 Toto Electric Industry Co. Control apparatus for mortar compounding apparatus
US4126181A (en) * 1977-06-20 1978-11-21 Palmer Engineering Company Ltd. Method and apparatus for formation fracturing with foam having greater proppant concentration
US4176064A (en) * 1977-06-20 1979-11-27 Palmer Engineering Company Ltd. Mixture concentrator
US4209258A (en) * 1978-02-14 1980-06-24 Oakes W Peter Automatic continuous mixer apparatus
US4265262A (en) * 1979-03-19 1981-05-05 William Hotine Fluent material level control system
US4327759A (en) * 1979-08-24 1982-05-04 Wimpey Laboratories Limited Slurry producing apparatus
US4265266A (en) * 1980-01-23 1981-05-05 Halliburton Company Controlled additive metering system
US4353482A (en) * 1980-01-23 1982-10-12 Halliburton Company Additive metering control system
US4298288A (en) * 1980-01-25 1981-11-03 Anthony Industries, Inc. Mobile concreting apparatus and method
US4436431A (en) * 1981-05-11 1984-03-13 William A. Strong Slurry production system
US4456069A (en) * 1982-07-14 1984-06-26 Vigneri Ronald J Process and apparatus for treating hydrocarbon-bearing well formations
US4538222A (en) * 1983-04-06 1985-08-27 Halliburton Company Apparatus and method for mixing a plurality of substances
US4474204A (en) * 1983-07-22 1984-10-02 The Western Company Of North America Delivery and metering device control system
US4475818A (en) * 1983-08-25 1984-10-09 Bialkowski Wojciech L Asphalt coating mix automatic limestone control
US4701095A (en) * 1984-12-28 1987-10-20 Halliburton Company Transportable material conveying apparatus
US4726219A (en) * 1986-02-13 1988-02-23 Atlantic Richfield Company Method and system for determining fluid pressures in wellbores and tubular conduits
US4665982A (en) * 1986-06-26 1987-05-19 Brown Billy R Formation fracturing technique using liquid proppant carrier followed by foam
US4779186A (en) * 1986-12-24 1988-10-18 Halliburton Company Automatic density control system for blending operation
US4845981A (en) * 1988-09-13 1989-07-11 Atlantic Richfield Company System for monitoring fluids during well stimulation processes
US4911241A (en) * 1989-01-27 1990-03-27 Dowell Schlumberger Incorporated Constant viscosity foam
US4887670A (en) * 1989-04-05 1989-12-19 Halliburton Company Controlling fracture growth
US4930576A (en) * 1989-04-18 1990-06-05 Halliburton Company Slurry mixing apparatus
US5281023A (en) * 1989-08-02 1994-01-25 Stewart & Stevenson Services, Inc. Method and apparatus for automatically controlling a well fracturing operation
US5114239A (en) * 1989-09-21 1992-05-19 Halliburton Company Mixing apparatus and method

Non-Patent Citations (22)

* Cited by examiner, † Cited by third party
Title
"Technique Helps Extend Cotton Valley Frac," Thomas M. Hopkins, II, T. M. Hopkins, Inc., Audis Byrd and R. E. Hyden, Halliburton Services.
Block Diagram, Stewart & Stevenson Services, Inc. *
Document relating to communications between assignee Stewart & Stevenson and National Petroleum Services Co., dated Nov. 16, 1993, 1 p. *
Documents relating to communications between assignee Stewart & Stevenson, and Globe Oilwell Services, Inc., 2 pp. *
Documents relating to communications between assignee Stewart & Stevenson, and Servicios Especiales San Antonio, S.A., 2 pp. *
Documents relating to communications between assignee, Stewart & Stevenson, and Dowell Schlumberger. *
Frac/Blender Unit Lightweight, Automated, Stewart & Steven Services, Inc. *
Introduction to Petroleum Production, Vol. 1, Chapter 4; D. R. Skinner; Well Completions; Gulf Publishing Co., 1981; (pp. 69 95). *
Introduction to Petroleum Production, Vol. 1, Chapter 4; D. R. Skinner; Well Completions; Gulf Publishing Co., 1981; (pp. 69-95).
Offshore Technology Conference, 1992; Automatic Control of Bulk Cement Tank Levels by D. A. Wienck, et al; (pp. 737 740). *
Offshore Technology Conference, 1992; Automatic Control of Bulk Cement Tank Levels by D. A. Wienck, et al; (pp. 737-740).
Offshore Technology Conference, 1992; Automatic Density Control and High Specific Mixing Energy Deliver Consistent High Quality Cement Slurries by C. Stegemoeller, et al; (pp. 725 736). *
Offshore Technology Conference, 1992; Automatic Density Control and High Specific Mixing Energy Deliver Consistent High-Quality Cement Slurries by C. Stegemoeller, et al; (pp. 725-736).
Precision Meets Dependability for the Perfect Mix (Dowell Schlumberger Advertisement). *
Sales information relating to present invention. *
Society of Petroleum Engineers, 1990; New Slurry Mixer Improves Density Control in Cementing Operations by E. O Neill, et al. *
Society of Petroleum Engineers, 1990; New Slurry Mixer Improves Density Control in Cementing Operations by E. O'Neill, et al.
Society of Petroleum Engineers, 1991; Process Control of Slurry Density: Impact on Field Performance of Slurry Density by R. J. Hitt, et al; (pp. 519 527). *
Society of Petroleum Engineers, 1991; Process Control of Slurry Density: Impact on Field Performance of Slurry Density by R. J. Hitt, et al; (pp. 519-527).
Technical Paper; Cement Mixing: Better Understanding and New Hardware by Galiana, et al; reprinted from Oilfield Review 3, No. 2 (Apr. 1991): 11 21. *
Technical Paper; Cement Mixing: Better Understanding and New Hardware by Galiana, et al; reprinted from Oilfield Review 3, No. 2 (Apr. 1991): 11-21.
Technique Helps Extend Cotton Valley Frac, Thomas M. Hopkins, II, T. M. Hopkins, Inc., Audis Byrd and R. E. Hyden, Halliburton Services. *

Cited By (52)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050166961A1 (en) * 1998-12-21 2005-08-04 Baker Hughes Incorporated Closed loop additive injection and monitoring system for oilfield operations
US7389787B2 (en) 1998-12-21 2008-06-24 Baker Hughes Incorporated Closed loop additive injection and monitoring system for oilfield operations
GB2361730A (en) * 1998-12-21 2001-10-31 Baker Hughes Inc Closed loop chemical injection and monitoring system for oilfield operations
GB2361730B (en) * 1998-12-21 2003-05-07 Baker Hughes Inc Closed loop chemical injection and monitoring system for oilfield operations
US6851444B1 (en) 1998-12-21 2005-02-08 Baker Hughes Incorporated Closed loop additive injection and monitoring system for oilfield operations
WO2000037770A1 (en) * 1998-12-21 2000-06-29 Baker Hughes Incorporated Closed loop chemical injection and monitoring system for oilfield operations
WO2001003842A1 (en) * 1999-07-13 2001-01-18 Hacking Earl L Jr Apparatus for sorting and recombining minerals
US6085912A (en) * 1999-07-13 2000-07-11 Hacking, Jr.; Earl L. Apparatus for sorting and recombining minerals background of the invention
US7037724B2 (en) 2000-10-17 2006-05-02 Baker Hughes Incorporated Method for storing and transporting crude oil
US20080023200A1 (en) * 2004-01-16 2008-01-31 Reddy B Raghav Settable Fluids Comprising Particle-Size Distribution-Adjusting Agents and Methods of Use
US7328756B2 (en) 2004-01-16 2008-02-12 Halliburton Energy Serivces, Inc. Settable fluids comprising particle-size distribution-adjusting agents and methods of use
US20050155795A1 (en) * 2004-01-16 2005-07-21 Reddy B. R. Settable fluids comprising particle-size distribution-adjusting agents and methods of use
US20050155763A1 (en) * 2004-01-16 2005-07-21 Reddy B. R. Settable fluids comprising particle-size distribution-adjusting agents and methods of use
US20060272819A1 (en) * 2004-01-16 2006-12-07 Halliburton Energy Services, Inc. Methods of preparing settable fluids comprising particle-size distribution-adjusting agents, and associated methods
US20050161107A1 (en) * 2004-01-23 2005-07-28 Mark Turnbull Apparatus and method for loading concrete components in a mixing truck
US7686499B2 (en) * 2005-04-14 2010-03-30 Halliburton Energy Services, Inc. Control system design for a mixing system with multiple inputs
US7308379B2 (en) 2005-04-14 2007-12-11 Halliburton Energy Services, Inc. Methods and systems for estimating density of a material in a mixing process
US20060231259A1 (en) * 2005-04-14 2006-10-19 Halliburton Energy Services, Inc. Method for servicing a well bore using a mixing control system
US20060235627A1 (en) * 2005-04-14 2006-10-19 Halliburton Energy Services, Inc. Methods and systems for estimating density of a material in a mixing process
US7543645B2 (en) 2005-04-14 2009-06-09 Halliburton Energy Services, Inc. Method for servicing a well bore using a mixing control system
US7353874B2 (en) 2005-04-14 2008-04-08 Halliburton Energy Services, Inc. Method for servicing a well bore using a mixing control system
US20060233039A1 (en) * 2005-04-14 2006-10-19 Halliburton Energy Services, Inc. Control system design for a mixing system with multiple inputs
US20080164023A1 (en) * 2005-04-14 2008-07-10 Halliburton Energy Services, Inc. Method for Servicing a Well Bore Using a Mixing Control System
US7494263B2 (en) 2005-04-14 2009-02-24 Halliburton Energy Services, Inc. Control system design for a mixing system with multiple inputs
US20090118866A1 (en) * 2005-04-14 2009-05-07 Halliburton Energy Services, Inc. Control System Design for a Mixing System with Multiple Inputs
US20080053220A1 (en) * 2006-09-06 2008-03-06 Allen Thomas E Method for determining absolute density of cement slurry
US20080053221A1 (en) * 2006-09-06 2008-03-06 Allen Thomas E Method for determining absolute density of cement slurry
US7614276B2 (en) 2006-09-06 2009-11-10 Allen Thomas E Method for determining absolute density of cement slurry
US7600414B2 (en) 2006-09-06 2009-10-13 Allen Thomas E Method for determining absolute density of cement slurry
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US20110166689A1 (en) * 2008-05-23 2011-07-07 Kevin Odell Alden Concrete material dispensing system
US9678496B2 (en) * 2008-05-23 2017-06-13 Amtec Meter & Controls, Inc. Concrete material dispensing system
US8863833B2 (en) 2008-06-03 2014-10-21 Baker Hughes Incorporated Multi-point injection system for oilfield operations
US20090294123A1 (en) * 2008-06-03 2009-12-03 Baker Hughes Incorporated Multi-point injection system for oilfield operations
US8523493B2 (en) 2008-12-17 2013-09-03 Johan Gunther Modified storage pod and feeding system for binder utilized for in-situ pilings and method of utilizing the same
US20100329797A1 (en) * 2008-12-17 2010-12-30 James M. Duncan Modified Storage Pod and Feeding System for Binder Utilized for In-Situ Pilings and Method of Utilizing the Same
US20100172202A1 (en) * 2009-01-08 2010-07-08 Halliburton Energy Services, Inc. Mixer system controlled based on density inferred from sensed mixing tub weight
US8177411B2 (en) 2009-01-08 2012-05-15 Halliburton Energy Services Inc. Mixer system controlled based on density inferred from sensed mixing tub weight
US8901217B2 (en) 2009-07-01 2014-12-02 Bridgestone Corporation Multiple-acid-derived metal soaps incorporated in rubber compositions and method for incorporating such soaps in rubber compositions
US20110039994A1 (en) * 2009-07-01 2011-02-17 Xiaorong Wang Multiple-Acid-Derived Metal Soaps Incorporated In Rubber Compositions And Method For Incorporating Such Soaps In Rubber Compositions
US8389609B2 (en) 2009-07-01 2013-03-05 Bridgestone Corporation Multiple-acid-derived metal soaps incorporated in rubber compositions and method for incorporating such soaps in rubber compositions
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US20110060062A1 (en) * 2009-09-10 2011-03-10 Bridgestone Corporation Compositions and method for making hollow nanoparticles from metal soaps
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